US5345896A - Method and apparatus for circulating solid material in a fluidized bed reactor - Google Patents

Method and apparatus for circulating solid material in a fluidized bed reactor Download PDF

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Publication number
US5345896A
US5345896A US08/041,580 US4158093A US5345896A US 5345896 A US5345896 A US 5345896A US 4158093 A US4158093 A US 4158093A US 5345896 A US5345896 A US 5345896A
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United States
Prior art keywords
chamber
particles
particle
reactor
particle chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US08/041,580
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English (en)
Inventor
Timo Hyppanen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Amec Foster Wheeler Energia Oy
Original Assignee
Ahlstrom Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ahlstrom Corp filed Critical Ahlstrom Corp
Priority to US08/041,580 priority Critical patent/US5345896A/en
Assigned to A. AHLSTRON CORPORATION reassignment A. AHLSTRON CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HYPPANEN, TIMO
Priority to US08/089,810 priority patent/US5840258A/en
Priority to US08/131,852 priority patent/US5406914A/en
Priority to KR1019950704214A priority patent/KR100321604B1/ko
Priority to ES94910430T priority patent/ES2129633T3/es
Priority to EP94910430A priority patent/EP0692997B1/fr
Priority to RU95117993/12A priority patent/RU2141870C1/ru
Priority to DE69416305T priority patent/DE69416305T2/de
Priority to EP98100452A priority patent/EP0844022A3/fr
Priority to PL94310975A priority patent/PL183100B1/pl
Priority to CA002158846A priority patent/CA2158846C/fr
Priority to AT94910430T priority patent/ATE176178T1/de
Priority to PCT/FI1994/000112 priority patent/WO1994022569A1/fr
Priority to JP6521703A priority patent/JPH08508440A/ja
Priority to AT94911965T priority patent/ATE146377T1/de
Priority to DK94911965T priority patent/DK0692999T4/da
Priority to ES94911965T priority patent/ES2098130T5/es
Priority to KR1019950704216A priority patent/KR100271621B1/ko
Priority to PCT/FI1994/000132 priority patent/WO1994022571A1/fr
Priority to PL94310977A priority patent/PL175242B1/pl
Priority to DE69401203T priority patent/DE69401203T3/de
Priority to EP94911965A priority patent/EP0692999B2/fr
Priority to CN94105284A priority patent/CN1079935C/zh
Priority to JP6521722A priority patent/JP2939338B2/ja
Priority to CA002158272A priority patent/CA2158272C/fr
Priority to EE9400016A priority patent/EE03097B1/xx
Publication of US5345896A publication Critical patent/US5345896A/en
Application granted granted Critical
Priority to US08/340,875 priority patent/US5772969A/en
Priority to FI954375A priority patent/FI119974B/fi
Priority to FI954373A priority patent/FI954373A/fi
Assigned to FOSTER WHEELER ENERGIA OY reassignment FOSTER WHEELER ENERGIA OY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: A. AHLSTROM CORPORATION
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
    • F22B31/0007—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus with combustion in a fluidized bed
    • F22B31/0084—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus with combustion in a fluidized bed with recirculation of separated solids or with cooling of the bed particles outside the combustion bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
    • F22B31/0007—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus with combustion in a fluidized bed
    • F22B31/0084—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus with combustion in a fluidized bed with recirculation of separated solids or with cooling of the bed particles outside the combustion bed
    • F22B31/0092—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus with combustion in a fluidized bed with recirculation of separated solids or with cooling of the bed particles outside the combustion bed with a fluidized heat exchange bed and a fluidized combustion bed separated by a partition, the bed particles circulating around or through that partition
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00—Fluidised bed combustion apparatus
    • F23C10/02—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2206/00—Fluidised bed combustion
    • F23C2206/10—Circulating fluidised bed
    • F23C2206/101—Entrained or fast fluidised bed
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2206/00—Fluidised bed combustion
    • F23C2206/10—Circulating fluidised bed
    • F23C2206/103—Cooling recirculating particles

Definitions

  • the present invention refers to a method and an apparatus for circulating solid material in a fluidized bed reactor, including a reactor chamber, having side walls defining the interior of the reactor chamber and a grid at the bottom of the reactor chamber; a gas discharge opening adjacent the upper end of the reactor chamber and a fluidized bed of solid particles in said reactor chamber, the fluidized bed having an internal circulation of solid particles.
  • a method for circulating solid material in a fluidized bed reactor, having an internal circulation of solid particles in which the following steps are practiced: (a) Classifying solid particles in the internal circulation by arranging a particle chamber in the fluidized bed of solid particles, the particle chamber having at least one barrier wall having openings allowing only solid particles of a size smaller than a predetermined size to flow from the fluidized bed through the barrier wall into the particle chamber. (b) Guiding large objects, having a size bigger than the predetermined size of particles, downwardly in the reactor chamber externally of the particle chamber. And, (c) recirculating at least a portion of the particles from the particle chamber into the reactor chamber.
  • the reactor comprises the following elements: A particle chamber arranged in the fluidized bed of solid particles; the particle chamber having a barrier wall provided with openings, such as holes or slots, preventing solid particles of a size bigger than a predetermined size from flowing from the reactor chamber into the particle chamber; and, the particle chamber further having a wall provided with at least one opening for recirculating particles from the particle chamber into the reactor chamber.
  • heat transfer surfaces are arranged in the particle chamber. Heat is then easily and efficiently recovered from particles without large objects adversely affecting heat recovery.
  • the particle chamber may be arranged adjacent to a side wall or a partition wall in the lower part of the reactor chamber for classifying solid particles flowing downwardly by gravity along the walls. Then the uppermost end or roof construction of the particle chamber may form a barrier wall therein.
  • the barrier wall may be horizontal or inclined.
  • the barrier wall having openings allowing only particles of a size smaller than a predetermined size to flow therethrough, prevents large objects from flowing into the particle chamber. By making the barrier wall inclined, e.g. about 30°-45° from horizontal the large objects are caused to continue to flow downwardly along the external side of the barrier wall without clogging the openings in the barrier wall.
  • a side wall of the particle chamber may in some embodiments form the barrier wall therein. Then particles having a horizontal momentum can flow through the openings in the barrier wall into the particle chamber.
  • the present invention may be used e.g. in fluidized bed combustors, where one or several particle chambers are arranged on the bottom of the combustion chamber.
  • the particle chamber or chambers may be adjacent the side walls or partition walls in the combustion chamber or may even stand freely on the bottom.
  • particle chambers may be arranged as protrusions higher up in the combustion chamber.
  • the particle chambers are arranged adjacent one or several of the reactor chamber side walls, then a portion of the vertical or inclined side wall may form a common wall between the particle chamber and the reactor chamber.
  • the particle chamber may be arranged on the inside or on the outside of the side wall part, which forms the common wall. Thereby the particle chamber may form a protrusion on the inside or outside of the reactor chamber. If the particle chamber forms a protrusion on the outside of the reactor chamber side wall, then the openings allowing particles to flow into the particle chamber are advantageously made in the portion of the side wall forming a common wall between the fine material chamber and the reactor chamber.
  • the particle chamber may be constructed of water tube panels as is the reactor chamber itself.
  • the tube panels may be refractory lined.
  • the openings in the wall forming the barrier wall may then be made in fins combining adjacent water tubes or may be made by bending a water tube or two adjacent water tubes to provide a slot between the tubes.
  • a furrow may be formed in the refractory lining and the openings may be made in the bottom plane of the furrow.
  • There may be only one opening or slot in a barrier wall if the amount of particles flowing through this opening is sufficient. Usually several openings or slots are arranged in the barrier wall for securing a sufficient flow of particles.
  • Slots or rows of openings arranged in horizontal or inclined walls on top of the particle chamber may advantageously be arranged perpendicularly to the reactor side wall.
  • the slots or rows of holes are preferably arranged vertically, but may in some embodiments be arranged horizontally.
  • the particle chamber may e.g. reach to a level 3 to 8 meters above the grid of a circulating fluidized bed reactor, so that a rather large downwards flow of particles may be caught by the particle chamber.
  • the openings in the barrier wall may in a circulating fluidized bed combustor be holes, having a diameter smaller than about 50 mm, preferably about 30 mm or smaller, or a slot having a width smaller than about 50 mm, preferably approximately 30 mm or smaller.
  • Such openings allow only approx. round particles of a size ⁇ 50 mm, preferably smaller than 30 mm, or oblong particles having a width ⁇ 50 mm, or preferably smaller than 30 mm, to flow through the barrier wall.
  • the particle chamber may be used for heat recovery. Then evaporators, superheaters or other heat transfer surfaces are arranged in the particle chamber.
  • the invention provides a possibility to run combustors at low load, even when it is impossible to get enough heating capacity in the upper regions of the combustor chamber or in external heat exchangers. The invention makes it possible to obtain a balance between superheating and evaporation for different loads or for different fuels.
  • Heat transfer surfaces may be arranged in any conventional manner in the particle chamber.
  • the heat transfer may be controlled by introducing fluidizing air/gas into the fine material chamber.
  • the fluidizing air may be used as secondary air in the combustion chamber.
  • a good mixing of solid material in the particle chamber is important if heat is to be recovered from the particles therein. This can be emphasized, if desired, by arranging the inlet or inlets and outlet or outlets of solid particles in opposite ends of the particle chamber.
  • particles are recirculated from the particle chamber back into the reactor chamber.
  • the particles may be recirculated by overflow through one or several openings in the particle chamber.
  • the openings may be arranged on one side wall of the particle chamber or there may be openings on several side walls. It is in most cases advantageous to arrange the openings far away from the inlet openings in the barrier wall, if a good mixing of particles in the particle chamber is desired.
  • the particles may alternatively be recirculated through a gas lock, such as narrow slot like openings disposed one above the other in a side wall in the particle chamber.
  • the particles may also be recirculated through a gas lock of an L-valve type formed between the particle chamber and the reactor chamber.
  • the recirculation may be controlled by fluidizing fine particles in the vicinity of the gas lock.
  • the particles may of course also be recirculated into the reactor chamber by mechanical means, such as a screw feeder.
  • Fluidizing air introduced into the combustor, for control of heat transfer or for transporting particles into the particle chamber, may be used as secondary air in the combustion chamber.
  • the particle outlet openings or the particle inlet openings allow gas to flow outward through the barrier wall countercurrently to the particle flow.
  • the particle flow inward into the particle chamber is unstable and does not prevent gases from escaping out from the chamber.
  • a circulating fluidized bed reactor bed material is discharged with the exhaust gases and separated from the gases in a particle separator.
  • the particles are thereafter reintroduced through a particle inlet into the reactor chamber, usually into the lower part of the reactor chamber.
  • the externally circulated bed material may be wholly or partly reintroduced into the reactor through that particle chamber.
  • An inlet for externally circulated material is then provided in the particle chamber. If heat transfer surfaces are to be arranged in the particle chamber, then heat is recovered from both externally and internally circulating material.
  • FIG. 1 is a schematic vertical cross sectional view of a circulating fluidized bed reactor constructed in accordance with a first preferred exemplary embodiment of the present invention
  • FIGS. 2 and 3 are schematic enlarged cross sectional views of the lower part of a fluidized bed reactor chamber according to other exemplary embodiments of the present invention.
  • FIG. 4 is a schematic isometric view of the lower part of a fluidized bed reactor chamber according to still another exemplary embodiment of the present invention.
  • FIGS. 5 and 6 are schematic enlarged views of the barrier walls in particle chambers according to other further embodiments of the present invention.
  • FIG. 7 is a perspective view, partly in cross section, of the barrier wall in FIG. 6.
  • FIG. 1 shows a circulating fluidized bed reactor 10 having a reactor chamber 12, a conventional windbox 14 with grid 15 for introducing fluidizing air into the reactor chamber 12, a conventional particle separator 16, a conventional gas outlet 18 and a conventional return duct 20 for recycling solid particles into the reactor chamber 12.
  • a particle chamber 22 according to the present invention is disposed in the lower part 24 of the reactor chamber 12.
  • the particle chamber 12 is provided in connection with an inlet 26 for particles being recycled through the return duct 20.
  • an inlet 26 for particles being recycled is introduced into the particle chamber 22.
  • a barrier wall 30 forming the roof of the particle chamber 22. Openings 32 in barrier wall 30 allow fine solid particles (see arrows 34) to flow through the barrier wall 30. Larger objects (see arrows 36) flow downwardly on the outside surface 37 of the particle chamber 22. The particles entering inlet 26 and openings 32 are reintroduced into the lower part of the reactor chamber through opening 38.
  • the opening 38 for reintroducing particles into the reactor chamber may constitute a gas lock, if necessary.
  • the opening 38 may, e.g., be formed by narrow slots disposed on top of the other, with each slot forming an L-valve.
  • Heat transfer surfaces 40 are disposed in the particle chamber 22.
  • the heat transfer surfaces 40 may e.g. be evaporator or superheater surfaces.
  • FIG. 2 shows an enlarged view of the lower part 124 of another embodiment of reactor chamber according to the invention.
  • particle chamber 122 is disposed adjacent a side wall 129 opposite to side wall 128 having the inlet 126 for recycled fine solid particles.
  • the particle chamber 122 is disposed in the lowermost part 124 of the reactor chamber, which has inclined refractory lined walls 41.
  • a portion 42 of the refractory lined wall 41 adjacent side wall 129 forms a side wall of the fine material chamber 122 as well.
  • the barrier wall 130 and side wall 137 of chamber 122 are preferably refractory lined.
  • the barrier wall 130 and the side wall 137 form a partition between the bottom 124 of the reactor chamber, and the particle chamber 122.
  • Heat transfer surfaces 140 are preferably disposed in the particle chamber 122. Heat transfer may be controlled by controlling the flow of fluidizing air from windbox 46, which opens into chamber 122. Also reintroduction of particles through opening 138 into the reactor chamber 112 may be controlled by controlling the flow of fluidizing air from windbox 114 in the vicinity of the opening 138.
  • FIG. 3 illustrates a further embodiment of the present invention.
  • the particle chamber 222 is provided as a portion of the inclined refractory lined wall element 242 of the lower reactor chamber 224.
  • Inlet openings 232 having a predetermined diameter or width are provided in the upper part of the refractory lined side wall portion 242, this upper part thereby forming a barrier wall 230.
  • Outlet openings 238 are provided in the lowermost part of the refractory lined side wall 241 for reintroducing particles into the reactor chamber. Solid particles flow into the particle chamber 222 through openings 232 and are recycled into the reactor chamber through openings 238. Some particles may be discharged from chamber 222 through an outlet 48 if desired.
  • FIG. 4 shows an isometric view of still another embodiment according to the present invention.
  • components comparable to those in FIG. 3 are shown by the same two digit reference numeral only preceded by a "3".
  • the inlet openings 332 and outlet openings 338 are in opposite parts of the particle chamber 322 for providing good mixing of the material therein.
  • the outlet opening 338 allows solid particles to flow from the particle chamber 322 into the reactor chamber 312.
  • the particle level in the particle chamber 322 is dependent on the location of the outlet opening 338 in wall 337.
  • FIGS. 5 and 6 show enlarged views of the barrier wall 330 of the reactor of FIG. 4.
  • the barrier wall holes 50 in FIG. 5 and slots 52 in FIG. 6 are made in furrows 54 in the refractory layer 56 covering the side walls 337 and the roof 330 of the particle chamber 332.
  • the particle chamber 322 walls may be made of tube panels, i.e. water or evaporator tubes connected by fins.
  • the furrows 54 in the embodiment shown in FIGS. 5 and 6 are made so as to expose the fins between the water or evaporator tubes. Openings 50 or slots 52 are formed in the fins.
  • the barrier wall 330 has ridgelike inclined surfaces 57 between the furrows 54 without any noticeable horizontal plane.
  • all particles flowing down onto the barrier wall 330 are guided towards the slots 52 in the bottom of the furrows 54.
  • Particles are gathered from a cross sectional area which is much greater than the cross sectional area of the slots.
  • Particles are gathered from a cross sectional area at least twice the area of the slots 52.
  • the ridges 57 make it possible to gather and classify particles from a large area without having to increase the size or amount of slots 52.
  • portions of the upper wall (30, 130, etc.) of the particle chamber (22, 122, etc.) may also form guide walls guiding particles towards the opening or slots.
  • FIG. 7 is a partly cross sectional view of the ridgelike elements 57 of the barrier wall 330 of FIG. 6.
  • the ridgelike elements 57 are made of tubeplate V-form sections 60, 62 covered with refractory 63.
  • the tubeplate is made of tubes 64 connected by fins 66.
  • the tubeplate sections are disposed parallel to each other, leaving a slot 52 between two adjacent sections 60, 62.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
US08/041,580 1992-11-10 1993-04-05 Method and apparatus for circulating solid material in a fluidized bed reactor Expired - Lifetime US5345896A (en)

Priority Applications (29)

Application Number Priority Date Filing Date Title
US08/041,580 US5345896A (en) 1993-04-05 1993-04-05 Method and apparatus for circulating solid material in a fluidized bed reactor
US08/089,810 US5840258A (en) 1992-11-10 1993-07-12 Method and apparatus for transporting solid particles from one chamber to another chamber
US08/131,852 US5406914A (en) 1992-11-10 1993-10-05 Method and apparatus for operating a circulating fluidized bed reactor system
RU95117993/12A RU2141870C1 (ru) 1993-04-05 1994-03-28 Способ и устройство для циркуляции твердого вещества в реакторе с псевдоожиженным слоем
ES94910430T ES2129633T3 (es) 1993-04-05 1994-03-28 Procedimiento para la circulacion de material solido en un reactor de lecho fluidizado.
EP94910430A EP0692997B1 (fr) 1993-04-05 1994-03-28 Procede permettant de faire circuler du materiau solide dans un reacteur a lit fluidise
KR1019950704214A KR100321604B1 (ko) 1993-04-05 1994-03-28 유동상반응기내의고체물질을순환시키는방법및장치
DE69416305T DE69416305T2 (de) 1993-04-05 1994-03-28 Methode zum zirkulieren von feststoff in einem wirbelschichtreaktor
EP98100452A EP0844022A3 (fr) 1993-04-05 1994-03-28 Appareil permettant de faire circuler du matériau solide dans un réacteur à lit fluidisé
PL94310975A PL183100B1 (pl) 1993-04-05 1994-03-28 Urządzenie do cyrkulacji materiału stałego w reaktorze ze złożem fluidalnym
CA002158846A CA2158846C (fr) 1993-04-05 1994-03-28 Methode et installation pour la mise en circulation de matieres solides dans un reacteur a lit fluidise
AT94910430T ATE176178T1 (de) 1993-04-05 1994-03-28 Methode zum zirkulieren von feststoff in einem wirbelschichtreaktor
PCT/FI1994/000112 WO1994022569A1 (fr) 1993-04-05 1994-03-28 Procede et appareil permettant de faire circuler du materiau solide dans un reacteur a lit fluidise
JP6521703A JPH08508440A (ja) 1993-04-05 1994-03-28 流動床反応炉での固体物質を循環する方法および装置
ES94911965T ES2098130T5 (es) 1993-04-05 1994-04-05 Sistema reactor de lecho fluidizado y procedimiento de fabricacion del mismo.
JP6521722A JP2939338B2 (ja) 1993-04-05 1994-04-05 流動床反応装置およびその製造方法
AT94911965T ATE146377T1 (de) 1993-04-05 1994-04-05 Wirbelbettreaktorsystem und methode zu dessen herstellung
KR1019950704216A KR100271621B1 (ko) 1993-04-05 1994-04-05 유동상 반응기 시스템 및 그 제조방법
PCT/FI1994/000132 WO1994022571A1 (fr) 1993-04-05 1994-04-05 Systeme de reacteur a lit fluidise et procede de fabrication
PL94310977A PL175242B1 (pl) 1993-04-05 1994-04-05 Reaktor ze złożem fluidalnym
DE69401203T DE69401203T3 (de) 1993-04-05 1994-04-05 Wirbelbettreaktorsystem und methode zu dessen herstellung
EP94911965A EP0692999B2 (fr) 1993-04-05 1994-04-05 Systeme de reacteur a lit fluidise et procede de fabrication
CN94105284A CN1079935C (zh) 1993-04-05 1994-04-05 用于使流化床反应器中的固体物料循环的方法和设备
DK94911965T DK0692999T4 (da) 1993-04-05 1994-04-05 Reaktorsystem med fluidiseret leje og fremgangsmåde til fremstilling af samme
CA002158272A CA2158272C (fr) 1993-04-05 1994-04-05 Reacteur a lit fluidise; methode de fabrication
EE9400016A EE03097B1 (et) 1992-11-10 1994-07-07 Meetod ja seade tahkete osakeste transportimiseks ühest kambrist teise kambrisse.
US08/340,875 US5772969A (en) 1992-11-10 1994-12-06 Method and apparatus for recovering heat in a fluidized bed reactor
FI954375A FI119974B (fi) 1993-04-05 1995-09-18 Leijukerrosreaktorijärjestelmä ja menetelmä sen valmistamiseksi
FI954373A FI954373A (fi) 1993-04-05 1995-09-18 Menetelmä ja laitteisto kiinteän aineen kierrättämiseksi leijukerrosreaktorissa

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/041,580 US5345896A (en) 1993-04-05 1993-04-05 Method and apparatus for circulating solid material in a fluidized bed reactor

Related Child Applications (3)

Application Number Title Priority Date Filing Date
US08/089,810 Continuation-In-Part US5840258A (en) 1992-11-10 1993-07-12 Method and apparatus for transporting solid particles from one chamber to another chamber
US08/131,852 Continuation-In-Part US5406914A (en) 1992-11-10 1993-10-05 Method and apparatus for operating a circulating fluidized bed reactor system
US14934293A Continuation-In-Part 1992-11-10 1993-11-09

Publications (1)

Publication Number Publication Date
US5345896A true US5345896A (en) 1994-09-13

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EP (2) EP0692997B1 (fr)
JP (1) JPH08508440A (fr)
KR (1) KR100321604B1 (fr)
CN (1) CN1079935C (fr)
AT (1) ATE176178T1 (fr)
CA (1) CA2158846C (fr)
DE (1) DE69416305T2 (fr)
ES (1) ES2129633T3 (fr)
PL (1) PL183100B1 (fr)
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Cited By (11)

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US5540894A (en) * 1993-05-26 1996-07-30 A. Ahlstrom Corporation Method and apparatus for processing bed material in fluidized bed reactors
WO1996033369A1 (fr) * 1995-04-21 1996-10-24 Foster Wheeler Energia Oy Centrale a cycle combine presentant un reacteur a lit fluidise circulant
US6237541B1 (en) 2000-04-19 2001-05-29 Kvaerner Pulping Oy Process chamber in connection with a circulating fluidized bed reactor
EP0785821B2 (fr) † 1994-10-12 2001-11-28 Foster Wheeler Energia Oy Reacteur a lit fluidise circulant
ES2239863A1 (es) * 2001-07-17 2005-10-01 THE BABCOCK & WILCOX COMPANY Una caldera de lecho fluidificado circulante (cfb) con intercambiador de calor en lecho controlable.
US20070266915A1 (en) * 2006-05-18 2007-11-22 Metso Power Oy Partition wall structure of a furnace
US20110159180A1 (en) * 2008-04-28 2011-06-30 Francois Ledoux Method and device for processing of granules
WO2011104434A1 (fr) 2010-02-26 2011-09-01 Foster Wheeler Energia Oy Agencement de réacteur à lit fluidisé
CN106196037A (zh) * 2016-08-31 2016-12-07 自贡华西能源工业有限公司 一种用于cfb烟气发生设备的外循环系统
US10293378B2 (en) * 2015-02-06 2019-05-21 United Technologies Corporation Powder processing apparatus for classifying and degassing
WO2019122509A1 (fr) * 2017-12-19 2019-06-27 Valmet Technologies Oy Chaudière à lit fluidisé circulant à échangeur de chaleur de boucle d'étanchéité

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US8163200B2 (en) 2006-08-16 2012-04-24 Merck Patent Gesellschaft Mit Beschraenkter Haftung Cyclohexene compounds for liquid-crystalline mixtures
CN103528049B (zh) * 2013-10-14 2016-02-10 上海交通大学 生物质-水煤浆混烧的有机工质锅炉
CN103557518B (zh) * 2013-10-14 2016-02-10 上海交通大学 洗煤泥燃烧的有机工质锅炉
CN103528054B (zh) * 2013-10-14 2016-02-10 上海交通大学 市政污泥-水煤浆混烧的有机工质锅炉
CN103528051B (zh) * 2013-10-14 2016-08-10 上海交通大学 生物质-洗煤泥混烧的有机工质锅炉

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US3893426A (en) * 1974-03-25 1975-07-08 Foster Wheeler Corp Heat exchanger utilizing adjoining fluidized beds
US4335662A (en) * 1980-09-12 1982-06-22 Combustion Engineering, Inc. Solid fuel feed system for a fluidized bed
US4823740A (en) * 1986-01-21 1989-04-25 Ebara Corporation Thermal reactor
US5060599A (en) * 1986-06-12 1991-10-29 Gotaverken Energy Aktiebolag Method and reactor for combustion in a fluidized bed
US4813479A (en) * 1986-12-11 1989-03-21 Gotaverken Energy Ab Adjustable particle cooler for a circulating fluidized bed reactor
US5141708A (en) * 1987-12-21 1992-08-25 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having an integrated recycle heat exchanger
US4915061A (en) * 1988-06-06 1990-04-10 Foster Wheeler Energy Corporation Fluidized bed reactor utilizing channel separators
US5242662A (en) * 1989-05-18 1993-09-07 Foster Wheeler Energy Corporation Solids recycle seal system for a fluidized bed reactor
US5054436A (en) * 1990-06-12 1991-10-08 Foster Wheeler Energy Corporation Fluidized bed combustion system and process for operating same
US5069171A (en) * 1990-06-12 1991-12-03 Foster Wheeler Agency Corporation Fluidized bed combustion system and method having an integral recycle heat exchanger with a transverse outlet chamber
US5239946A (en) * 1992-06-08 1993-08-31 Foster Wheeler Energy Corporation Fluidized bed reactor system and method having a heat exchanger

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5540894A (en) * 1993-05-26 1996-07-30 A. Ahlstrom Corporation Method and apparatus for processing bed material in fluidized bed reactors
EP0785821B2 (fr) † 1994-10-12 2001-11-28 Foster Wheeler Energia Oy Reacteur a lit fluidise circulant
WO1996033369A1 (fr) * 1995-04-21 1996-10-24 Foster Wheeler Energia Oy Centrale a cycle combine presentant un reacteur a lit fluidise circulant
US6237541B1 (en) 2000-04-19 2001-05-29 Kvaerner Pulping Oy Process chamber in connection with a circulating fluidized bed reactor
US20010048901A1 (en) * 2000-04-19 2001-12-06 Alliston Michael G. Process chamber in connection with a circulating fluidized bed reactor
ES2239863A1 (es) * 2001-07-17 2005-10-01 THE BABCOCK & WILCOX COMPANY Una caldera de lecho fluidificado circulante (cfb) con intercambiador de calor en lecho controlable.
US20070266915A1 (en) * 2006-05-18 2007-11-22 Metso Power Oy Partition wall structure of a furnace
US9527104B2 (en) 2008-04-28 2016-12-27 Yara International Asa Method and device for processing of granules
US9199265B2 (en) 2008-04-28 2015-12-01 Yara International Asa Method and device for processing of granules
US20110159180A1 (en) * 2008-04-28 2011-06-30 Francois Ledoux Method and device for processing of granules
WO2011104434A1 (fr) 2010-02-26 2011-09-01 Foster Wheeler Energia Oy Agencement de réacteur à lit fluidisé
US9091481B2 (en) 2010-02-26 2015-07-28 Amec Foster Wheeler Energia Oy Fluidized bed reactor arrangement
EP2539635A4 (fr) * 2010-02-26 2017-03-22 Amec Foster Wheeler Energia Oy Agencement de réacteur à lit fluidisé
US10293378B2 (en) * 2015-02-06 2019-05-21 United Technologies Corporation Powder processing apparatus for classifying and degassing
CN106196037A (zh) * 2016-08-31 2016-12-07 自贡华西能源工业有限公司 一种用于cfb烟气发生设备的外循环系统
WO2019122509A1 (fr) * 2017-12-19 2019-06-27 Valmet Technologies Oy Chaudière à lit fluidisé circulant à échangeur de chaleur de boucle d'étanchéité
US11603989B2 (en) 2017-12-19 2023-03-14 Valmet Technologies Oy Circulating fluidized bed boiler with a loopseal heat exchanger

Also Published As

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CA2158846C (fr) 2002-07-30
PL310975A1 (en) 1996-01-22
DE69416305D1 (de) 1999-03-11
ES2129633T3 (es) 1999-06-16
EP0692997A1 (fr) 1996-01-24
EP0844022A3 (fr) 1998-07-01
CN1095461A (zh) 1994-11-23
JPH08508440A (ja) 1996-09-10
CA2158846A1 (fr) 1994-10-13
EP0692997B1 (fr) 1999-01-27
ATE176178T1 (de) 1999-02-15
EP0844022A2 (fr) 1998-05-27
DE69416305T2 (de) 1999-06-17
KR100321604B1 (ko) 2002-06-20
WO1994022569A1 (fr) 1994-10-13
KR960701690A (ko) 1996-03-28
PL183100B1 (pl) 2002-05-31
CN1079935C (zh) 2002-02-27
RU2141870C1 (ru) 1999-11-27

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